US5349046AExpiredUtility
Polymerization of β-lactones under rim conditions
Est. expiryDec 1, 2012(expired)· nominal 20-yr term from priority
C08G 63/823C08G 63/08
56
PatentIndex Score
9
Cited by
21
References
19
Claims
Abstract
A method is disclosed for making a molded article of manufacture of polymerized beta -lactone which method involves injecting into a mold at least one beta -lactone monomer and at least one nucleophilic initiator, substantially polymerizing the beta -lactone in the mold and removing the resultant polymerized article from the mold.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A method for making a molded article of manufacture comprising polymerized β-lactone which method comprises injecting into a mold at least one β-lactone monomer and from about 1.0×10 -8 to about 1.0×10 -1 by weight basis monomer of at least one nucleophilic initiator, polymerizing said β-lactone in said mold and removing the resultant polymerized article from the mold.
2. The method of claim 1 wherein the β-lactone has the formula: ##STR5## wherein R 1 , R 2 , R 3 and R 4 are individually hydrogen or hydrocarbyl of carbon number ranging from 1 to about 20.
3. The method of claim 2 wherein R 1 , R 2 , R 3 and R 4 are individually hydrogen or hydrocarbyl of carbon number ranging from 1 to about 6.
4. The method of claim 3 wherein the β-lactone monomer is selected from the group consisting of propiolactone, β-butyrolactone, pivalolactone and mixtures thereof.
5. The method of claim 1 wherein the nucleophilic initiator is one or more organic compounds of Group Va of the Periodic Table.
6. The method of claim 5 wherein the nucleophilic initiator is one or more compounds selected from the group consisting of amines, phosphines, arsines, stibenes, bismuthenes and mixtures thereof.
7. The method of claim 6 wherein the nucleophilic initiator has the general formula R 1 R 2 R 3 Z wherein Z is nitrogen or phosphorus and R 1 , R 2 and R 3 are hydrocarbyl of 1 to 10 carbon atoms.
8. The method of claim 6 wherein the nucleophilic initiator is selected from tertiary amines, tertiary phosphines and mixtures thereof.
9. The method of claim 1 wherein the initiator comprises from about 1.0×10 -7 to about 1.0×10 -2 mole % of monomer.
10. The method of claim 9 wherein the initiator comprises from about 1.0×10 -6 to about 1.0×10 -3 mole % of monomer.
11. The method of claim 1 wherein said mold is maintained at a temperature of from about 60° C. to about 120° C. prior to injection of monomer and initiator.
12. A polymer article of manufacture produced according to the method of claim 1 having a molecular weight of at least 20,000 as determined by low angle laser light scattering.
13. The polymer article of manufacture produced according to the method of claim 12 having a molecular weight of at least 30,000.
14. A polymer article of manufacture produced according to the method of claim 1 having crystallinity of greater than about fifty percent.
15. The polymer article of manufacture produced according to the method of claim 14 having a crystallinity of greater than about sixty percent.
16. The polymer article of manufacture produced according to the method of claim 16 having a crystallinity of greater than about seventy-five percent.
17. A method for making a molded article of manufacture comprising polymerized β-lactone which method comprises injecting into a mold at least one β-lactone monomer of the formula: ##STR6## wherein R 1 , R 2 , R 3 and R 4 are individually hydrogen or methyl and from about 0.01 to about 1 percent by weight basis monomer of at least one nucleophilic initiator selected from tertiary amines or tertiary phosphines, polymerizing said β-lactone in said mold and removing the resultant polymerized article from the mold.
18. The method of claim 17 wherein said initiator is selected from a compound having the general formula R 1 R 2 R 3 Z wherein Z is nitrogen or phosphorus and R 1 , R 2 and R 3 are hydrocarbyl of 1 to 10 carbon atoms.
19. The method of claim 17 wherein said mold is maintained at a temperature of from about 60° C. to about 120° C. prior to injection of monomer and initiator.Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.